Droplet ejecting coatings

ABSTRACT

Coating compositions are provided that eject droplets of condensed fluid from a surface. The coatings include a nanostructured coating layer and in some embodiments, also include a hydrophobic layer deposited thereon. The coating materials eject droplets from the surface in the presence of non-condensing gases such as air and may be deployed under conditions of supersaturation of the condensed fluid to be ejected. A heat exchanger design utilizing the coating is described herein.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a continuation of U.S. application Ser. No. 16/334,198, filed on Mar. 18, 2019, which is a U.S. national phase application under 35 U.S.C. § 371 of PCT/US2017/052119, filed on Sep. 19, 2017, which claims the benefit of U.S. Provisional Application Nos. 62/396,728, filed Sep. 19, 2016, and 62/397,319, filed Sep. 20, 2016, both of which are incorporated by reference herein in their entireties.

FIELD OF THE INVENTION

The invention relates to compositions that eject condensed fluids from a surface and methods of use thereof.

BACKGROUND

Water fouling is a common problem in condensation heat transfer applications. Hydrophobic coatings are currently used to promote dropwise condensation heat transfer, which has previously been shown to enhance heat transfer by as much as three-fold, relative to uncoated surfaces. Dropwise condensation typically involves droplets nucleating on the surface, coalescing, and sliding down the surface due to gravity. “Jumping droplet” condensation is a relatively new phenomenon that has been observed with only two hydrophobic surfaces in systems that contain only water vapor. Contrary to typical dropwise condensation, “jumping droplet” condensation involves droplets nucleating on the surface, growing through the further condensation of vapor and/or coalescence and then jumping from the surface out of plane. This has been shown to enhance the heat transfer as high as 35% over typical dropwise condensation. Non-condensing gases, such as air, have been observed to prevent the jumping droplet condensation; consequently, this phenomenon has never been observed in the presence of non-condensing gasses such as air. Furthermore, supersaturation above 1.12 has also observed to cause the droplets to flood the surface instead of jumping, resulting in reduced heat transfer relative to a typical hydrophobic surface. (Miljkovic, N., et al., Jumping-Droplet-Enhanced Condensation on Scalable Superhydrophobic Nanostrucutred Surfaces, Nano Lett. 13:179-187, doi:10.1021/n1303835d (2013); Miljkovic, N., et al., Modeling and Optimization of Superhydrophobic Condensation, J. Heat Transf-Trans. ASME 135:14, doi:10.1115/1.4024597 (2013); Milkovic, N., et al. Condensation heat transfer on superhydrophobic surfaces, MRS Bull. 38:397-406, doi:10.1557/mrs.2013.103 (2013); Aili, A., et al., in ASME 2016 5th International Conference on Micro/Nanoscale Heat and Mass Transfer, V001T004A001 (ASME, 2016))

One problem encountered in high efficiency HVAC applications is blowoff of condensed water vapor being entrained in the primary flow, such that corrosion and other undesirable outcomes occur. To combat corrosion of heat exchanger fins, barrier coatings are often employed. In order to maintain high water condensation efficiency (air side heat transfer efficiency), coatings which modify the surface energy (to be either hydrophobic or hydrophilic or even biphilic (patterned areas of hydrophobic and hydrophilic)) are applied. Hydrophilic coatings retain the condensate on the fins in a thin layer, so as to minimize downstream blowoff. Hydrophobic coatings are designed to rapidly shed condensate from the surface.

Improved surface structures that promote ejection of droplets for heat transfer and/or dehumidification, without the disadvantages of previous systems, are needed for high efficiency applications. Improved surface structures that promote ejection of droplets and increase overall heat transfer can lead to heat exchanger designs with improved overall efficiency, smaller overall footprint, simpler fin designs, or combinations of all of the above.

BRIEF SUMMARY OF THE INVENTION

Coating compositions for ejection of droplets of condensed liquid from a surface and methods of making and using such compositions are provided herein.

The coating compositions include a nanostructured layer deposited on a substrate, and a hydrophobic coating deposited on the nanostructured layer. The texture and/or geometry of the nanostructured layer provides a driving force for droplet ejection.

In one aspect, coating compositions are provided that are deposited on a substrate. The coating ejects droplets of a condensate from the substrate in the presence of a gas mixture that includes one or more non-condensing gas (NCG). In some embodiments, the gas mixture comprises, consists of, or consists essentially of air or the primary molecular constituents of air. In some embodiments, the condensate comprises, consists of, or consists essentially of water.

In some embodiments, the coating ejects droplets of a condensate from the substrate under condensing conditions, wherein the condensate is formed at supersaturation, for example, above about 1.1. In some embodiments, the coating ejects droplets of a condensate from the substrate under condensity conditions, wherein the droplet arithmetic mean diameter of the ejected droplets is less than about 500 micrometers.

In some embodiments, the coating includes a layer of a nanostructured coating material. In some embodiments, the nanostructured coating material is hydrophobic. In other embodiments, the coating includes a hydrophobic functional layer deposited or layered over at least a portion of the nanostructured coating material.

In another aspect, methods of making a coating composition that ejects droplets of a condensate from a substrate under condensing conditions are provided. In some embodiments, the methods include depositing a nanostructured coating material on a substrate, wherein the coating material is textured such that droplets are ejected from the surface of the coating material. For example, the coating may be textured such that droplets are ejected when the cohesive forces (e.g., surface tension force) exceed the surface tension adhesion forces, thereby resulting in a net force vector with a component directed away from the substrate, e.g., out of the plane of the substrate. In some embodiments, the nanostructured coating material is hydrophobic. In other embodiments, the method further includes depositing or layering a hydrophobic functional on the surface of at least a portion of the nanostructured coating material.

In another aspect, a method for removal of a condensate from a surface is provided. In some embodiments, the method includes exposing a substrate that includes a coated substrate (a substrate that includes a coating composition on a surface of the substrate) to a condensing substance, under conditions in which condensation of the substance occurs, wherein fluid droplets (condensed droplets) of the substance are formed on the surface and the surface ejects the droplets. In some embodiments, the coated substrate includes a nanostructured coating material, e.g., a layer of a nanostructured coating material deposited on the substrate. In some embodiments, the nanostructured coating material is hydrophobic. In other embodiments, the coating includes a hydrophobic functional layer deposited or layered over at least a portion of the nanostructured coating material.

In some embodiments, the droplets are ejected in the presence of one or more NCG. In some embodiments, the coating ejects droplets in the presence of a gas mixture that includes one or more NCG. In some embodiments, the gas mixture comprises, consists of, or consists essentially of air or the primary molecular constituents of air. In some embodiments, the condensed droplets comprise, consist of, or consist essentially of water.

In some embodiments, the droplets that are ejected from the substrate are formed at supersaturation, for example, above about 1.1. In some embodiments, the droplets that are ejected from the substrate have a droplet arithmetic mean diameter less than about 500 micrometers.

In some embodiments, the coated substrate is exposed to a gas mixture, such as air, that includes particulate material, e.g., air that includes particulates, and the method include collection of the particulate material, e.g., airborne particulates, in the ejected droplets, thereby removing the particulate material, e.g., airborne particulates, from the gas mixture, e.g., air.

In another aspect, methods for heat transfer are provided, wherein the coating compositions described herein are exposed to a condensing substance under conditions in which the substance condenses as droplets on the surface of the composition, and wherein the droplets are ejected from the surface. The methods may include exposure of the coating composition to the condensing substance in the presence of one or more non-condensing gases (NCG(s)), such as air, component(s) of air, and/or inert gas(es). The methods may include condensation of the condensing substance under conditions of supersaturation, for example, supersaturation above about 1.0, about 1.1, or about 1.25. In some embodiments, the condensing substance is water, ethanol, or a refrigerant substance, or a mixture thereof.

In another aspect, heat exchangers are provided. Heat exchangers can be designed to utilize the coatings described herein and address the primary problems of fouling, efficiency and corrosion. Aluminum fins are typically used in the volume manufacture of heat exchangers owing to their low cost and high performance. The methods described herein address the application of nanostructured coatings to this construction material. Also described herein are heat exchanger designs that benefit from the implementation of the disclosed coatings and operation in a jumping droplet mode of condensation. Close fin spacing of at least about or greater than about 4 fins per inch, 8 fins per inch, 10 fins per inch, 12 fins per inch, 14 fins per inch, 16 fins per inch, 18 fins per inch, 20 fins per inch, 22 fins per inch, 24 fins per inch, 30 fins per inch, or greater permit effective heat transfer and high condensate collection efficiency. Fin spacing as measured as the distance between the fins may be as low as about 25 microns, 50 microns, 75 microns, 100 microns, 200 microns, 400 microns, 800 microns, 1200 microns, 1600 microns, 2000 microns, or 5000 microns. In this design, a fin coated with a nanostructured coating described herein is placed in close proximity to one or more additional fins. The fins may be coated with either hydrophobic, droplet ejection coatings as described herein, or with hydrophilic materials such as the base coating as described herein. Small droplets that are ejected from the surface and that are too small to impinge upon the adjacent surface are vaporized downstream, and heat transfer to these droplets causes their evaporation, with the latent heat being removed and further reducing the air temperature. Droplets that impinge upon adjacent plates may be collected and removed from the system through a condensate collection system. In certain nonlimiting embodiments, droplets are collected downstream from the droplet ejection surfaces.

In another aspect, heat exchangers are provided. In some embodiments, heat exchangers are provided that include a droplet ejection coating material as described herein. In some embodiments, a heat exchanger further includes one or more hydrophilic surface(s). Droplets may be ejected from the droplet ejection coating and collected by the hydrophilic surface. In some embodiments, adjacent surfaces of the heat exchanger are coating with droplet ejection coating material and the remaining surfaces are hydrophilic. In some embodiments, condensate droplets are formed at supersaturation, for example, above about 1.1. In some embodiments, droplets are ejected at an arithmetic mean droplet diameter less than about 500 micrometers. In some embodiments, the temperature of the surface of the heat exchanger is reduced below the freezing point of the condensate.

BRIEF DESCRIPTION OF THE DRAWINGS

FIGS. 1(a)-1(b) show highly magnified darkfield images of uncoated aluminum (1(a)) and aluminum coated with a droplet ejection coating as described in Example 1 (1(b)), after 12 hours under condensing conditions with water. The image appears to show significantly less water condensed on the coated surface of 1(b), but this is not the case. The water condensed and was rapidly ejected from the surface before the droplets reached a measurable size as observed through a microscope. Using the method described in Example 1, the water droplets were ejected at an average diameter of less than 500 micrometers.

FIGS. 2(a 1)-2(a 5) and 2(b 1)-2(b 5) show highly magnified darkfield images showing the progression of condensation on both uncoated aluminum (2(a 1)-2(a 5)) and aluminum coated with a droplet ejection coating as described in Example 1 (2(b 1)-2(b 5)). As time progressed on the uncoated aluminum surface (2(b 1)→2(b 2)→2(b 3)→2(b 4)→2(b 5)), droplets nucleated and coalesced into larger droplets. These droplets gravitationally drained by running down the surface. This process then repeats to remove water from a stream of NCGs. As time progresses on the surface coated with the droplet ejection coating, the droplets nucleate, grow, and eject from the surface before they can become large enough to be drained by gravity. This results an increased exposed area on the heat transfer surface, thus increasing overall heat transfer efficiency

FIGS. 3(a 1)-3(a 3), 3(b 1)-3(b 3), and 3(c 1)-3(c 3) show highly magnified darkfield image progressions of sub-millimeter droplets ejecting out of plane of the condensing surface described in Example 1. Sequential frames are from videos of a vertical plate recorded at 52 frames per second. The droplets ejected orthogonal to the gravity vector and then fell downward due to gravity and moved to the right due to the airflow in a controlled wind tunnel designed to simulate the environment inside of an air conditioning system. The camera was oriented 20 degrees to the vertical such that a narrow strip of the substrate was in the focal plane. The degree of supersaturation varied from 1 to 2 with no loss of performance. The inset scale bars in 3(b 1) and 3(b 2) are 250 μm and the inset scale bars in 3(c 1) and 3(c 2) are 100 μm. As the time progresses from 1 to 2 to 3, the step between each image is about 0.02 seconds. The droplet ejecting in 3(b) is about 120 μm while the droplets ejecting in 3(c) are about 10 to 20 μm. As time progresses on each shown droplet ejection from 3(a 1)→3(a 2)→3(a 3), 3(b 1)→3(b 2)→3(b 3), and 3(c 1)→3(c 2)→3(c 3). The droplets can be seen on the surface in 3(a 1), 3(b 1), and 3(c 1). 20 milliseconds later, the droplet can be observed leaving the surface in 3(a 2), 3(b 2), and 3(c 2). The ejection event happens in a small fraction of a second as 3(a 3), 3(b 3), and 3(c 3) indicate the droplet has cleared the field of view of the microscope. These ejection events happen many thousands of times per second; these three events are only an example of the phenomenon.

FIGS. 4a-4b show a schematic representation of a heat exchanger utilizing nanostructured coatings as described herein. 4 a shows an arrangement of fins with alternating droplet ejection and hydrophilic coatings. 4 b shows a schematic arrangement of heat exchanger fins with a droplet ejection coated area upstream and a hydrophilic coated area downstream from the heat exchanger fluid circulation tube in cross section. The figures are not meant to be final design configurations, but rather to schematically convey concepts described herein.

FIGS. 5a-5d show the onset of the freezing process on the uncoated panel (left) and liquid condensate on the treated panel (right).

DETAILED DESCRIPTION

The invention provides coating compositions and methods for efficient heat transfer by ejection of condensed liquid from a surface under condensing conditions. The compositions described herein include a nanostructured coating layer on a substrate, with a hydrophobic functional layer deposited on the nanostructured layer. The geometry of the nanostructured layer provides a driving force for ejection of droplets from the surface. The coating compositions described herein eject droplets of condensed liquid (e.g., water) from the surface in the presence of non-condensing gases (e.g., air or components thereof, or inert gases). In some embodiments, the condensed liquid is ejected from the surface at supersaturation greater than about 1, greater than about 1.1, greater than about 1.2, or greater than about 1.25. In some embodiments, the droplets are ejected from the surface with an arithmetic mean of diameters less than about 2000 microns, less than about 1500 microns, less than about 500 microns, less than about 250 microns, less than about 100 microns, less than about 75 microns, less than about 50 microns, less than about 25 microns, or less than about 10 microns. In some embodiments, the arithmetic mean of diameters is any of about 2000, 1500, 500, 250, 100, 75, 50, 25, or 10 microns to about 5 microns. Droplets may be ejected from the surface to enhance heat transfer, to affect ambient humidity, and/or to enhance dehumidification. In certain embodiments, the coating compositions described herein may be used in applications such as, but not limited to, water collection and purification, condensate collection, solvent and/or contaminant recovery, atomization, or humidification.

Definitions

Numeric ranges provided herein are inclusive of the numbers defining the range.

“A,” “an” and “the” include plural references unless the context clearly dictates otherwise.

A “nanostructured” coating refers to a coating composition that has a feature in at least one dimension that is less than 100 nanometers.

“Non-condensing gases” or “NCGs” refers to gasses that do not change phase at the desired condensing conditions of a vapor. Oxygen and nitrogen, for example, are NCGs when air is being dehumidified.

“Air” refers herein to a mixture of NCGs in a gaseous stream that also includes condensable materials such as water vapor, and other condensable components. For example, air may include, but is not limited to, oxygen, nitrogen, argon and/or other inert gas(es), and more easily condensable gases, such as water vapor and carbon dioxide. The primary molecular constituents of air are nitrogen, oxygen, argon, carbon dioxide, neon, helium, methane, and water vapor.

“Condensing conditions” refers to a condition wherein a surface is cooled below the dewpoint of a vapor.

“Supersaturation” refers to a condition when the vapor pressure of a vapor is above the equilibrium vapor pressure at a given temperature and pressure. A supersaturation of 1 refers to a relative humidity of 100% and any further increase promotes condensation.

“Ejection” in reference to droplets of liquid refers to leaving a surface with a velocity that has a non-zero normal component.

“Surface tension” refers to the tension of a liquid surface caused by cohesive forces in the bulk of the liquid that pulls inward toward the bulk and tends to minimize the surface area for a given volume.

“Droplet adhesion forces” refers to the forces responsible for causing a droplet to pull outward and spread on a surface, thus preventing it from forming a sphere. Contrarily, “cohesive forces” are those forces that cause a droplet to pull itself inward and form a sphere, such as surface tension.

“Refrigerant” refers to a substance or mixture used in a refrigeration cycle as the working fluid. This fluid often goes through phase changes, but need not to be effective.

“Working fluid” refers to a liquid or gas that absorbs or transmits energy. For example, the working fluid in an air conditioner system is the coolant such as Freon, glycol, or water that is used to cool the process fluid.

“Process fluid” refers to a liquid or gas that is being treated by interaction with the working fluid. For example, in an air conditioner system, the process fluid is the air that is being cooled.

“Sensible heat ratio” refers to the ratio of the sensible cooling capacity to the total cooling capacity.

Droplet Ejecting Coatings

Droplet ejecting coating materials are provided that eject condensed droplets of liquid from the surface of a substrate. The droplet ejecting coating material includes a nanostructured material deposited on a substrate, and a hydrophobic material deposited on the nanostructured material. The nanostructured material includes a geometry that provides a driving force for droplet ejection from the surface. The geometry may include, but is not limited to, a nanostructure that causes the droplets to take a distorted shape upon condensation.

Droplet ejecting coating materials may include a surface that is textured such that condensed droplets are ejected when the surface tension force exceeds the droplet adhesion forces, thereby resulting in a net force vector that has a component out of the plane of the substrate, for example, in applications in which the removal of the liquid from the surface or the inlet stream is advantageous. A surprising example of such an application is the prevention of freezing, i.e., prevention of onset of frost, for example, wherein the droplet diameter at ejection is sufficiently small, less than about 500 micrometers, which prevents frost and frost adhesion on substrates of interest.

The coating materials disclosed herein may eject condensed fluid from the surface in the presence of a gas mixture, e.g., a gas mixture that includes one or more NCGs. For example, the coating materials may eject fluid in the presence of air, gas components of air, or inert gases. In some embodiments, the gas mixture includes oxygen and/or nitrogen. In some embodiments, the gas mixture includes nitrogen, oxygen, carbon dioxide, hydrogen, helium, and argon, or combinations thereof. In one embodiments, the gas mixture consists of nitrogen, oxygen, carbon dioxide, hydrogen, helium, and argon. In some embodiments, the gas mixture includes oxygen, nitrogen, carbon dioxide, and argon, or combinations thereof. In one embodiment, the gas mixture consists of oxygen, nitrogen, carbon dioxide, and argon. In one embodiment, the gas mixture is air.

The coating materials disclosed herein may eject condensed fluid from the surface at supersaturation greater than about 1.0, 1.1, 1.2, or 1.25, or at supersaturation about 1.0 to about 1.1, about 1.1 to about 1.25, about 1.1 to about 3.0, or about 1.1 to 5.0.

Condensed fluid droplets that may be ejected by the coating materials disclosed herein include, but are not limited to, water, ethanol, and refrigerants. In some embodiments, the condensed fluid is selected from water, ethanol, a hydrofluorocarbon (HFC), and a hydrofluoro-olefin (HFO), or a combination thereof. In some embodiments, the condensed fluid is selected from water, ethanol, difluoromethane (HFC-32), difluoroethane (HFc-152a), pentafluoroethane (HFC-125), 2,3,3,3-tetrafluoropropene (HCO-1234yf), 1,3,3,3-tetrafluoropropene (HFO1234ze), or a combination thereof. In one embodiment, the condensed fluid is water. In some embodiments, the condensed fluid is an industrial process or working fluid.

Droplet ejecting coating materials as described herein may eject condensed fluid droplets from the surface having an arithmetic mean of diameters of less than about 2 millimeters, less than about 1 millimeter, less than about 500 microns, less than about 250 microns, less than about 100 microns, less than about 75 microns, less than about 50 microns, less than about 25 microns, or less than about 10 microns, or any of about 10 microns to about 25 microns, about 25 microns to about 50 microns, about 50 microns to about 75 microns, about 75 microns to about 100 microns, about 100 microns to about 250 microns, about 250 microns to about 500 microns, about 500 microns to about 1 millimeter, about 1 millimeter to about 2 millimeters, about 10 microns to about 50 microns, about 25 microns to about 100 microns, or about 100 microns to about 500 microns.

In some embodiments, the nanostructured coating layer includes nanostructured metal, ceramic, glass, or polymer.

In some embodiments, the nanostructured coating layer includes a ceramic that is a metal oxide. The metal oxide may be, for example, a transition metal oxide, tin(IV) oxide, magnesium (II) oxide (MgO), or aluminum oxide. In some embodiments, the transition metal oxide is selected from zinc oxide, iron(II, III) oxide (Fe₃O4), iron(III) oxide (Fe₂O₃), manganese(IV) oxide (MnO₂), manganese(II, III) oxide (Mn₃O₄), manganese(III) oxide (Mn₂O₃), nickel(II) oxide (NiO), nickel(III) oxide (Ni₂O₃), zirconium(IV) oxide (ZrO₂), titanium(IV) oxide (TiO₂), chromium(III) oxide (Cr₂O₃), copper(II) oxide (CuO), cobalt(II) oxide (CoO), cobalt(III) oxide (Co₂O₃), and cobalt(II, III) oxide (Co₃O₄).

In some embodiments, the nanostructured coating layer includes a glass. In some examples, the glass includes silica or a silicate.

In some embodiments, the nanostructured coating layer includes a polymer. In some examples, the polymer is a fluoropolymer, polyethylene, or polypropylene. In some embodiments, the polymer is a fluoropolymer selected from polytetrafluoroethylene (PTFE), polyvinylidene (PVDF), polyvinylfluoride (PVF), and fluorinated ethylene propylene (FEP), or a combination thereof. In some embodiments, the polymer is a block copolymer, for example, but not limited to, wherein each block of the copolymer is less than about 500 monomer units, or less than about 200 monomer units. For example, the block copolymer may by a hydrophobic polymer that includes two or more monomer units. In some embodiments, the block co-polymer may include one or more monomers, such as, but not limited to, propylene, ethylene, tetrafluoroethylene, trifluoroethylene, vinylfluoride, hexafluoropropoylene, 1,1-difluoroethylene, 1,2-difluoroethylene, and isobutylene.

In some embodiments, the hydrophobic coating layer may include one or more hydrophobic functionality selected from alkyl, vinyl, phenyl, and fluoroalkyl. For example, the hydrophobic functionality may include, but is not limited to, alkylsilane, vinylsilane, phenylsilane, or fluoroalkylsilane. In certain nonlimiting embodiments, the hydrophobic functionality is hexamethyldisilazine, sodium methylsiliconate, potassium methylsiliconate, dimethiconol, perfluorooctyltriethoxysilane, perfluorodecyltriethoxysilane, perfluorooctyltrimethoxysilane, perfluorodecyltrimethoxysilane, octadecyltriethoxysilane, methyltrimethoxysilane, methyltriethoxysilane, isobutyltrimethoxysilane, isobutyltriethoxysilane, or phenyltriethoxysilane. In some embodiments the hydrophobic coating refers to a functionalized perfluoropolyether such as perfluoropolyether silane, perfluoropolyether phosphonic acid, or perfluoropolyether phosphonate. In some embodiments, the hydrophobic coating refers to a coating that when added to a smooth substrate, imparts a contact angle greater than or equal to 90 degrees.

Methods of Making Droplet Ejection Coatings

Methods of making coatings that eject droplets of condensed liquid from a substrate, e.g., under condensing conditions, are provided. In some embodiments, the methods include: (a) depositing a nanostructured coating layer on a substrate; and (b) depositing a hydrophobic functional layer, i.e., a hydrophobic material that includes one or more hydrophobic functional groups, on the surface of the nanostructured material. In other embodiments, the methods include: depositing a layer of nanostructured coating material on a substrate, wherein the nanostructured coating material is hydrophic or includes one or more hydrophobic functional groups on its surface.

The nanostructured layer may be deposited on the substrate by any suitable means, including but not limited to, sol gel processing, chemical bath deposition, dip coating, spray coating, physical vapor deposition, or chemical vapor deposition. In one embodiment, the nanostructured coating is a metal oxide that is deposited by, for example, sol gel processing, chemical bath deposition, or dip coating. The hydrophobic functional layer may be deposited onto the nanostructured layer by any suitable means, including but not limited to, vapor deposition or dip coating.

Nonlimiting examples of nanostructured and hydrophobic coating materials are described above. The substrate may include a metal, metal alloy, glass, polymer or ceramic material.

In some embodiments, the substrate is pretreated prior to deposition of a nanostructure coating layer as described herein, to remove debris or substance(s) on the surface and/or to smooth the surface (i.e., to access the substrate to promote adhesion and to prevent defects), with one or more treatment(s) selected from cleaning, degreasing, rinsing, etching, desmutting, oxidizing, removing previous treatments, roughening, planarizing, steam cleaning, thermal oxidation, and smoothing.

Methods of Using Droplet Ejecting Coatings

Methods of using coatings as described herein for removal of fluid from surface, for heat removal, for removal of airborne particulate and contaminants, for dehumidification, and/or for the prevention of frosting are also provided. The methods include exposing a substrate with a droplet ejecting coating thereon, as described herein, to a condensing substance, under conditions in which condensation of the substance occurs, wherein fluid droplets of the substance are formed on the surface, and wherein the surface ejects the droplets. In some embodiments, the methods include (a) depositing a nanostructured coating layer on a substrate; and (b) depositing a hydrophobic functional layer on the surface of the nanostructured material, and (c) exposing the coated substrate to a condensing substance, under conditions in which condensation of the substance occurs, wherein fluid droplets of the substance are formed on the surface, and wherein the surface ejects the droplets.

In some embodiments, exposing the coated substrate to the condensing substance occurs in the presence of one or more gases, e.g., comprising or consisting of one or more NCGs. In one example, the coated substrate is exposed to the condensing substance in the presence of air. In some embodiments, the coated substrate is exposed to the condensing substance in the presence of a gas mixture that includes one or more of nitrogen, oxygen, carbon dioxide, hydrogen, helium, and argon, or a combination thereof. In some embodiments, the quantity of the gas mixture to which the coated substrate is exposed may be, for example, about 1 ppb to about 10 ppm, greater than about 5 ppm, greater than about 1%, or greater than about 20%, or in certain embodiments up to 100%, for example, to separate water vapor from an air stream, or to separate condensable substance(s) from a gas stream.

In some embodiments, exposing the coated substrate to the condensing substance occurs at supersaturation of the substance. In one example, the supersaturation is greater than about 1.1. In some embodiments, the supersaturation is greater than any of about 1.0, 1.1, 1.2, or 1.25, or is about 1.0 to about 1.1, about 1.1 to about 1.25, about 1.1 to about 3.0, or about 1.1 to about 5.0

In some embodiments, the substrate may be used in a working environment with no external electric field or bias.

The condensing substance may be any substance that condenses on a surface and that is desired to be removed from the surface, for example, for purposes of reducing the temperature at which onset of condensation occurs or to increase the amount of condensation that occurs at a given temperature. For example, the condensing substance may be water, ethanol, or a refrigerant. In one embodiment, the condensing substance is water vapor. In some embodiments, the droplets that are ejected may change the properties of an industrial process or working fluid.

The condensing substance may be any substance that condenses or adheres on a surface and that is desired to be removed from the surface, for example, for the purposes preventing the formation of adhered frost or ice on the surface. For example, the condensing substance may be water, wherein the surface temperature is below the freezing point of water, and the water is removed from the surface prior to the formation of the solid phase (frost or ice). In another embodiment, the condensing substance may be water, wherein the surface temperature is below the freezing point of water, and the liquid droplet ejects partially from a wetted to a dewetted state, which depresses the apparent freezing point of the liquid.

In some embodiments, the coatings described herein enhance the efficiency of a distillation system, e.g., a vapor distillation device, by increasing the condensation temperature, thereby reducing the energy requirements for the distillation system.

In some embodiments, the coatings described herein reduce the energy requirements for condensation in process equipment, such as, for example, a condenser, e.g., a distillation reflux condenser.

In some embodiments, the coatings described herein increase the condensation performance in process equipment, such as, for example, a vent gas stream, e.g., a knock-out pot.

In some embodiments, an external force, e.g., air flow, vibration, and/or droplet coalescence, provides excess energy in addition to the surface tension, to effect droplet ejection.

In some embodiments, ejected condensate droplets may be directed and collected. For example, an external collection unit or part, e.g., an adjacent external collection unit or part, may be used to collect condensed, ejected liquid. Examples of such a collection unit or part include, but are not limited to, a heat exchanger (e.g., heat exchanger fin), a screen, a filter, a mist collector, and a condensate collection pan.

In some embodiments, droplets are ejected into a cooled gas mixture stream, e.g., a gas mixture stream that includes one or more NCG, e.g., air, and revaporized, thus decreasing the temperature of a working or industrial process fluid. For example, droplets ejected into the cooled gas mixture stream may vary the sensible heat ratio of the cooled working or industrial process fluid. In one embodiment, the condensing substance is water and the working or process fluid is air, and the relative humidity is increased and the temperature is decreased, thus increasing the sensible heat capacity of the heat exchanger.

In some embodiments, ejected droplets will interact with airborne particulate and collect this material to the droplet. Several droplets can be collected in a variety of ways and the collected particulate can be removed from the system.

In some embodiments, ejected droplets will interact with airborne compounds. Airborne compounds which are soluble in the ejected droplet material will be solubilized and collected by the ejected droplets. Airborne compounds which are capable of suspension in the ejected droplet material will be suspended and collected by the ejected droplets. Several droplets can be collected in a variety of ways and the collected compounds can be removed from the system. For example, ejected water droplets may collect additional droplets of airborne substances or facilitate heterogeneous condensation.

Heat Exchanger Designed for Use with Droplet Ejecting Coating

A system. that includes alternating fins of hydrophilic and hydrophobic (e.g., droplet ejection) coatings and methods of making same are provided. Hydrophilic coating areas can be generated in conjunction with the hydrophobic (e.g., droplet ejection) coatings described herein by submerging and processing alternate fins separately and reassembling, or generating adjacent areas of droplet ejection and hydrophilic properties by partially submerging the part to be coated after the initial deposition of the nanostructured coating. A previously assembled unit may be partially coated with hydrophobic (e.g., droplet ejection) coating upstream and remain hydrophilic downstream, via partial submersion during the coating process. An assembled unit may be coated with a hydrophilic material, and subsequently partially coated with a hydrophobic coating.

A structure in which alternating fins are coated with hydrophobic (e.g., droplet ejection) and hydrophilic material is described. Condensate formed on hydrophilic coated fins wicks water, for return to a condensate drip pan. Condensate formed on hydrophobic (e.g., droplet ejection) material coated fins ejects condensate, to be collected on adjacent fins or collection apparatus for return to a condensate drip pan.

A heat exchanger or other system in which some areas (e.g., upstream areas) are coated with hydrophobic (e.g., droplet ejection) materials and other areas (e.g., downstream areas) are hydrophilic is described. In some embodiments, condensate formed on droplet ejection coated areas and ejected may be collected by downstream hydrophilic materials. In some embodiments, any part of the heat exchanger from which droplets are to be ejected may be coated with droplet ejection material as described herein, and remaining parts that will collect the condensate may be a hydrophilic material. For example, the chassis, drip pan, etc. may be coated with the droplet ejection) material, in addition to, or alternatively to, fins. In some embodiments, adjacent surfaces of the heat exchanger are coated with droplet ejection (e.g., hydrophobic) coating and the remaining surfaces are hydrophilic. In some embodiments the hydrophilic material is a coating, and in other embodiments the surface is inherently hydrophilic or is rendered hydrophilic by a surface treatment.

A system that includes fins that include droplet ejection coatings and methods of making the same are provided. A structure in which fins are coated with droplet ejection material is described. Condensate formed on droplet ejection material coated fins ejects condensate, to be collected for removal. Condensate formed on droplet ejection coated areas and ejected may be collected by downstream hydrophilic materials. In some embodiments, any part of the system (e.g, heat exchanger) from which droplets are to be ejected may be coated with droplet ejection material as described herein, and remaining parts that will collect the condensate may be a hydrophilic material. For example, the chassis, drip pan, etc. may be coated with the droplet ejection material, in addition to, or alternatively to, fins. In some embodiments, the hydrophilic material is a coating, and in other embodiments the surface is inherently hydrophilic or is rendered hydrophilic by a surface treatment. In other embodiments, ejected condensate coalesces naturally (e.g. droplet-droplet) or actively (e.g. mesh screen coalescer) and is removed by gravity or other accelerations of the gas mixture stream (e.g., cyclone or bend in stream).

Heat Exchanger Designed for Use with Droplet Ejecting Coating for Antifrost

A heat exchanger or other system that reduces or eliminates frost formation, and methods of making the same, are provided. Such a system that includes a droplet ejection coating material as described herein, and frost formation is reduced or eliminated in comparison with an identical system that does not include the droplet ejection coating material. Condensate formed on surfaces that contain the droplet ejection coating is removed via the droplet ejection mechanism described herein. A structure in environmental surface temperatures and conditions in which condensate retained on the surface would eventually form a solid frost or ice ejects droplets of the condensate via the droplet ejection mechanism as described herein, thereby delaying or preventing altogether the formation of solid frost or ice. The formation of frost and ice is detrimental to the efficiency of such devices and additional equipment, and methods and materials described herein are used to remove or prevent formation of the frost and/or ice. Structures that include droplet ejection coatings also reduce the time and/or energy required to remove frost and/or ice. Systems may be designed using the droplet ejection coating materials described herein to minimize energy use for defrosting and/or deicing. For example, the defrosting cycle may be optimized for energy minimization. For example, the defrosting system and hardware may be modified for energy minimization (e.g., lower power) and/or removed altogether.

The following examples are intended to illustrate, but not limit, the invention.

EXAMPLES Example 1

Droplet ejecting coatings were created by submerging a cleaned substrate in an aqueous equimolar solution of an alkaline earth metal or transition metal salt and hexamine with concentrations ranging from 10 mM to 1 M for a time ranging from 5 minutes to 3 hours. For example, an aluminum substrate was used with zinc nitrate as the transition metal salt at a concentration of 50 mM, and a temperature of 90° C. for duration of 2 hours. The substrate was then removed from the solution, rinsed, and air dried. The coated substrate was then baked at a temperature ranging from 100° C. to 600° C. for a duration ranging from 5 minutes to 48 hours. For example, the coating was baked at a temperature of 550° C. for a duration of 24 hours. The surface was then submerged in a dilute acid rinse solution between the pH of 1 and 7 for a duration ranging from 15 seconds to 24 hours. For example, the substrate was submerged in an acid solution at a pH of 3 for 24 hours. The substrate was then placed in a solution containing the hydrophobic functional molecule at a concentration ranging from 0.05% to 2% for a duration ranging from 2 seconds to 48 hours. For example, a 1% solution of perfluorodecyltriethoxysilane was created in azeotropic ethanol. A few drops of acetic acid were added to catalyze the reaction. The substrate was then submerged in the solution for 24 hours, rinsed, and then annealed at 120° C. for an hour. The substrate was then cooled in a stream of supersaturated air to eject droplets from the surface.

Results are shown in FIGS. 1(a)-1(b), FIGS. 2(a 1)-2(a 5) and 2(b 1)-2(b 5), and FIGS. 3(a 1)-3(a 3), 3(b 1)-3(b 3), and 3(c 1)-3(c 3).

Example 2

A droplet ejecting coating is created by dipping a cleaned substrate in a solution of a block copolymer consisting of two or more monomers with at least one of the monomers capable of being formed into a hydrophobic polymer. For example, a 1% solution of poly(tetrafluoroethylene-block-ethylene) is created using a solvent or solvent mixture. The polymer block length can range from 50 to 500 monomer units, such as a length of 500 monomer units. For example, the solvent is a Vertrel/trichlorobenzene mixture in a 50/50 ratio. The substrate is then removed and allowed to dry. The substrate is then cooled in a stream of supersaturated air to eject water droplets from the surface.

Example 3

A droplet ejecting coating is created by dipping a cleaned substrate with a roughened texture in a solution of a block copolymer consisting of two or more monomers with at least one of the monomers capable of being formed into a hydrophobic polymer. For example, the substrate is dipped into a melt of block copolymer of fluorinated ethylene propylene (FEP) wherein the polymer block lengths can range from 50 to 500 monomer units, such as a length of 500 monomer units. No solvent is required as the coating is formed from the melt. The substrate is then cooled in a stream of the super saturated air to eject water droplets from the surface.

Example 4

A 200 aluminum mesh of 5056 aluminum alloy was coated conformally using the process as described in Example 1, leaving the open area largely unchanged. The mesh had the following characteristics:

Mesh Size 200 × 200 Opening Size 0.0029″ (75 microns) Open Area 34% Wire Diameter 0.0021″ (53 microns)

Example 5

A 1 inch (in.)×2 in. 3003 aluminum alloy panel was coated conformally using the process as described in Example 1. A similar 1 in.×2 in. 3003 aluminum alloy panel was untreated. The panels were mounted to an electrically cooled module in a side by side fashion. The temperature of the cooled module was reduced to the point where condensation was observed and droplet ejection condensation was noted on the treated panel. Condensation was noted on the untreated panel. The cooled module temperature was further reduced to approximately 5° F. of subcooling, and freezing of the droplets was observed on the untreated panel, whereas freezing did not occur on the treated panel.

FIGS. 5a-5d show the onset of the freezing process on the uncoated panel and liquid condensate on the treated panel.

Although the foregoing invention has been described in some detail by way of illustration and examples for purposes of clarity of understanding, it will be apparent to those skilled in the art that certain changes and modifications may be practiced without departing from the spirit and scope of the invention. Therefore, the description should not be construed as limiting the scope of the invention.

All publications, patents, and patent applications cited herein are hereby incorporated by reference in their entireties for all purposes and to the same extent as if each individual publication, patent, or patent application were specifically and individually indicated to be so incorporated by reference. 

We claim:
 1. A heat exchanger that comprises coated surfaces, wherein the coated surfaces comprise a nanostructured coating material deposited on regions of a metal surface of the heat exchanger and a hydrophobic functional layer coated over the nanostructured coating material, wherein when the heat exchanger is in operation and is exposed to a process fluid under conditions in which condensation of at least a portion of condensable components in the process fluid occurs, droplets of a condensate from the condensable components are formed on the coated surfaces and the coated surfaces eject the droplets, and wherein the nanostructured coating material comprises a metal oxide that is deposited onto the metal surface of the heat exchanger without the introduction of an electric current.
 2. A heat exchanger according to claim 1, wherein the nanostructured coating material and the metal surface of the heat exchanger comprise different metals.
 3. A heat exchanger according to claim 1, further comprising one or more hydrophilic surface(s), wherein at least one hydrophilic surface is adjacent to at least one coated surface, wherein the adjacent coated surface is hydrophobic, and wherein when the heat exchanger is in operation, at least a portion of the droplets that are formed on the hydrophobic coated surface transfer to and traverse the hydrophilic surface as a liquid condensate.
 4. A heat exchanger according to claim 3, wherein the liquid condensate is collected by a downstream condensate collector.
 5. A heat exchanger according to claim 3, wherein the hydrophilic surface(s) comprise a nanostructured material.
 6. A heat exchanger according to claim 1, wherein the droplets are ejected in the presence of one or more non-condensing gas.
 7. A heat exchanger according to claim 1, wherein the droplets are ejected at supersaturation of the condensate above about 1.1.
 8. A heat exchanger according to claim 1, wherein the droplets are ejected at an arithmetic mean droplet diameter less than about 500 micrometers.
 9. A heat exchanger according to claim 1, wherein when the heat exchanger is in operation, frost formation on the heat exchanger is reduced or eliminated in comparison with a heat exchanger that does not comprise the coated surfaces.
 10. A heat exchanger according to claim 1, wherein the metal oxide of the nanostructured coating material comprises a transition metal oxide, tin (IV) oxide, magnesium (II) oxide, aluminum oxide, or an earth metal oxide.
 11. A heat exchanger according to claim 1, wherein the nanostructured coating material comprises zinc oxide, magnesium (II) oxide (MgO), iron (II, III) oxide (Fe₃O₄), iron (III) oxide (Fe₂O₃), manganese (IV) oxide (MnO₂), manganese (II, III) oxide (Mn₃O₄), manganese (III) oxide (Mn₂O₃), nickel (II) oxide (NiO), nickel (III) oxide (Ni₂O₃) chromium (III) oxide (Cr₂O₃), copper (II) oxide (CuO), cobalt (II) oxide (CoO), cobalt (III) oxide (Co₂O₃), or cobalt (II, III) oxide (Co₃O₄).
 12. A heat exchanger according to claim 1, wherein the hydrophobic functional layer comprises one or more hydrophobic functionality selected from alkyl, vinyl, phenyl, and fluoroalkyl.
 13. A heat exchanger according to claim 12, wherein the hydrophobic functional layer comprises alkylsilane, vinylsilane, phenylsilane, or fluoroalkylsilane.
 14. A heat exchanger according to claim 1, wherein the nanostructured coating material is immobilized on the metal surface of the heat exchanger by heat treatment at a temperature from 100° C. to 600° C.
 15. A heat exchanger according to claim 1, wherein the nanostructured coating material is deposited onto the metal surface of the heat exchanger in a solution comprising: an alkaline earth metal or a transition metal salt; and hexamine.
 16. A heat exchanger according to claim 1, wherein the metal surface of the heat exchanger comprises aluminum and the nanostructured coating material comprises zinc and/or manganese.
 17. A heat exchanger according to claim 1, wherein retention of the condensate on the heat exchanger surface is prevented when the temperature of the surface of the heat exchanger is below the dew point of the condensable components of the process fluid.
 18. A heat exchanger according to claim 1, wherein formation of adhered frost or ice on the coated surfaces is prevented when the temperature of the coated surfaces is below the freezing point of the condensable components of the process fluid.
 19. A heat exchanger that comprises coated surfaces, wherein the coated surfaces comprise a nanostructured coating material deposited on regions of a metal surface of the heat exchanger and a hydrophobic functional layer coated over the nanostructured coating material, wherein when the heat exchanger is in operation and is exposed to a process fluid under conditions in which condensation of at least a portion of condensable components in the process fluid occurs, droplets of a condensate from the condensable components are formed on the coated surfaces and the coated surfaces eject the droplets, further comprising one or more hydrophilic surface(s), wherein at least one hydrophilic surface is adjacent to at least one coated surface, wherein the adjacent coated surface is hydrophobic, and wherein when the heat exchanger is in operation, at least a portion of the droplets that are formed on the hydrophobic coated surface transfer to and traverse the hydrophilic surface as a liquid condensate.
 20. A heat exchanger according to claim 19, wherein the liquid condensate is collected by a downstream condensate collector.
 21. A heat exchanger according to claim 19, wherein the hydrophilic surface(s) comprise a nanostructured material.
 22. A heat exchanger that comprises coated surfaces, wherein the coated surfaces comprise a nanostructured coating material deposited on regions of a metal surface of the heat exchanger and a hydrophobic functional layer coated over the nanostructured coating material, wherein when the heat exchanger is in operation and is exposed to a process fluid under conditions in which condensation of at least a portion of condensable components in the process fluid occurs, droplets of a condensate from the condensable components are formed on the coated surfaces and the coated surfaces eject the droplets, and wherein the hydrophilic surface(s) comprise a nanostructured material.
 23. A heat exchanger that comprises coated surfaces, wherein the coated surfaces comprise a nanostructured coating material deposited on regions of a metal surface of the heat exchanger and a hydrophobic functional layer coated over the nanostructured coating material, wherein when the heat exchanger is in operation and is exposed to a process fluid under conditions in which condensation of at least a portion of condensable components in the process fluid occurs, droplets of a condensate from the condensable components are formed on the coated surfaces and the coated surfaces eject the droplets, and wherein the nanostructured coating material is deposited onto the metal surface of the heat exchanger in a solution comprising: an alkaline earth metal or a transition metal salt; and hexamine. 